EP0604708B1 - Fermentation method for the fast production of methane - Google Patents

Fermentation method for the fast production of methane Download PDF

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Publication number
EP0604708B1
EP0604708B1 EP19930113598 EP93113598A EP0604708B1 EP 0604708 B1 EP0604708 B1 EP 0604708B1 EP 19930113598 EP19930113598 EP 19930113598 EP 93113598 A EP93113598 A EP 93113598A EP 0604708 B1 EP0604708 B1 EP 0604708B1
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European Patent Office
Prior art keywords
methanosarcina
methane fermentation
substrate
methane
dsm
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EP19930113598
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German (de)
French (fr)
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EP0604708A1 (en
Inventor
Naoki Nakatsugawa
Koki Horikoshi
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Japan Science and Technology Agency
Mitsubishi Electric Corp
RIKEN Institute of Physical and Chemical Research
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Mitsubishi Electric Corp
Research Development Corp of Japan
RIKEN Institute of Physical and Chemical Research
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Priority claimed from JP63053294A external-priority patent/JPH01225480A/en
Priority claimed from JP5329588A external-priority patent/JPH0647120B2/en
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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/28—Anaerobic digestion processes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20—Bacteria; Culture media therefor
    • C12N1/205—Bacterial isolates
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P5/00—Preparation of hydrocarbons or halogenated hydrocarbons
    • C12P5/02—Preparation of hydrocarbons or halogenated hydrocarbons acyclic
    • C12P5/023—Methane
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12R—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
    • C12R2001/00—Microorganisms ; Processes using microorganisms
    • C12R2001/01—Bacteria or Actinomycetales ; using bacteria or Actinomycetales
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel

Definitions

  • the present invention relates to a methane fermentation method in which methanogenic bacteria are used and more specifically to a method for carrying out methane fermentation in a reactor for methane fermentation at a high speed within a short period of time in which the concentration of methanogenic bacteria is increased, and the best use of the properties of the methanogenic bacteria is made.
  • Methanosarcina barkeri see Microbiological Reviews, 1979, Vol. 47, pp. 260-296 and FEMS Microbiology Letters, 1983, Vol. 16, pp. 217-223); Methanosarcina acetivorans (see Applied and Environmental Microbiology, 1984, Vol. 47, No.5, pp. 971-978); Methanosarcina vacuolata (see Microbiology, U.S.S.R., 1979, Vol. 48, pp. 279-285); Methanosarcina thermophila (see International Journal of Systematic Bacteriology, 1985, Vol. 35, No.4, pp. 522-523); and Methanosarcina mazei (see Current Microbiology, 1980, Vol. 3, pp. 321-326). These species can be used for the method of the invention.
  • methane fermentation methods have been utilized widely for treating waste water and solid waste from the viewpoint of effective use of biomass, biogas production or the like.
  • the conventionally known methanogenic bacteria used in methane fermentation methods are strictly anaerobic bacteria and show an extremely slow growth rate. For this reason, the use of a large-scale reactor for methane fermentation is required and likewise it takes a long period of time to obtain in the reactor the concentration of the methanogenic bacteria which is required for maintaining a stable steady state of methane fermentation.
  • a method of methane fermentation utilizing organic waste characterized by using methane bacteria such as methanosulcina, methanococcus or methanobacterium and adding lower aliphatic acid or alcohol such as acetic acid, butyric acid, methyl alcohol or ethyl alcohol to the organic waste (see Patent Abstracts of Japan, 1980, Vol. 4, No. 19 (C-73)).
  • methane bacteria such as methanosulcina, methanococcus or methanobacterium
  • lower aliphatic acid or alcohol such as acetic acid, butyric acid, methyl alcohol or ethyl alcohol
  • the main substrates are acetic acid and H 2 /CO 2 (among the substrates capable of being assimlated by methanogens, acetic acid and H 2 /CO 2 are exclusively present in such waste).
  • the assimilation rate of acetic acid by methanogenic bacteria is very low and this serves as a rate-determining step.
  • the reactor is started according to the adaptation-cultivation method using substrates inherent to the bacteria used.
  • an object of the present invention is to provide a methane fermentation method which can provide methane at a high speed and high efficiency and which makes it possible to increase the bacterial concentration in a reactor within a short period of time, utilizing the bacteriological properties of methanogenic bacteria.
  • a methane fermentation method which comprises culturing at least one methanogenic bacterium in a culture medium, wherein the methanogenic bacterium is capable of assimilating one or more first substrates such as acetic acid, H 2 /CO 2 , or a mixture thereof at a low rate and a second substrate at a high rate, the culture medium containing one or more said first substrates and the culture being carried out in the additional presence of methylamine as the second substrate.
  • first substrates such as acetic acid, H 2 /CO 2 , or a mixture thereof at a low rate and a second substrate at a high rate
  • Fig. 1 is a diagram illustrating the change in the amount of methane gas generated with time.
  • Composition of the Solution of Trace Element Component Amount (g/l) Ferrous sulfate 0.3 Cobalt chloride 0.2 Zinc chloride 0.1 Boric acid 0.05 Sodium molybdate 0.2 Manganese chloride 0.1 Copper sulfate 0.01 Aluminum potassium sulfate 0.005 Nitrilotriacetic acid 2.5 Nickel chloride 0.5 Sodium selenite 0.1 Sodium tungstate 1.0 Cadmium chloride 0.05 *): Each numerical value in Table II denotes the content of each component per liter of the solution of trace elements in which the balance was purified water.
  • composition of the Solution of Vitamin Component Amount (mg/l) Biotin 2 Folic acid 2 Pyridoxine 10 Riboflavin 5 Thiamine 5 Pantothenic acid 5 Cyanocobalamin 0.1 p-Aminobenzoic acid 5 Alpha-lipoic acid 5 *):
  • Vitamin Component Amount (mg/l) Biotin 2 Folic acid 2 Pyridoxine 10 Riboflavin 5 Thiamine 5 Pantothenic acid 5 Cyanocobalamin 0.1 p-Aminobenzoic acid 5 Alpha-lipoic acid 5 *):
  • Each numerical value in Table III denotes the content of each component per liter of the solution of vitamins in which the balance was purified water.
  • methanogenic bacteria which are capable of utilizing at least two substrates and which utilize these substrates at different assimilation rates.
  • methanogenic bacteria examples include those belonging to the genus Methanosarcina . Specific examples of such: methanogenic bacteria are listed in the following Table IV.
  • the method of the present invention produces methane by culturing the aforementioned methanogenic bacteria in the presence of substrates as principal subject of fermentation which are assimilated by the bacteria at a low assimilation rate such as acetic acid, H 2 /CO 2 , or a mixture thereof and carrying out the culture or the fermentation in the presence of substrates which are assimilated at a low assimilation rate and of the substrate methylamine which is assimilated at a rate faster than that of the former.
  • substrates as principal subject of fermentation which are assimilated by the bacteria at a low assimilation rate such as acetic acid, H 2 /CO 2 , or a mixture thereof
  • Methanosarcina acetivorans C2A when Methanosarcina acetivorans C2A is cultured at a temperature of 35 to 40°C, the generation time thereof is 24.1 hours for acetic acid as a substrate; 5.2 hours for methanol; and 6.7 to 7.3 hours for methylamine.
  • acetic acid is used as the substrate which is assimilated at a low rate
  • methylamine is used as the substrate assimilated at a high rate.
  • the method of the present invention can likewise be carried out in the same manner as above, when Methanosarcina alkaliphilum , (whose generation time at 37°C is 19 hours for H 2 /CO 2 ; 17 hours for acetic acid; 4 hours for methanol; and 6 hours for methylamine) is used as the methanogenic bacterium.
  • Methanosarcina alkaliphilum (whose generation time at 37°C is 19 hours for H 2 /CO 2 ; 17 hours for acetic acid; 4 hours for methanol; and 6 hours for methylamine) is used as the methanogenic bacterium.
  • Methanosarcina alkaliphilum (whose generation time at 37°C is 19 hours for H 2 /CO 2 ; 17 hours for acetic acid; 4 hours for methanol; and 6 hours for methylamine) is used as the methanogenic bacterium.
  • H 2 /CO 2 acetic acid or a mixture thereof is used as the substrate which is assimilated at a low rate
  • the method of the present invention can be performed in the presence of one or more of the substrates such as acetic acid, H 2 /CO 2 or a mixture thereof which are assimilated at a low assimilation rate and of the substrate methylamine which is assimilated at a high assimilation rate, simultaneously.
  • the substrates such as acetic acid, H 2 /CO 2 or a mixture thereof which are assimilated at a low assimilation rate and of the substrate methylamine which is assimilated at a high assimilation rate, simultaneously.
  • the time for introducing, into a reaction system, the substrate assimilated at a high rate and the amount thereof may vary depending on factors such as the scale of the fermentation bath. For instance, the starting time of the reaction can extremely be reduced by adding it at the beginning of the fermentation.
  • Conditions of fermentation may appropriately be varied depending on the kinds of the methanogenic bacteria and the fermentation may be carried out according to conventional methods.
  • the method of the present invention can be applied to not only the methane fermentation in treating solid waste and waste water but also to the methane fermentation in all the other fields.
  • the methane fermentation method of the present invention makes it possible to increase the bacterial concentration of the methanogenic bacterium in a reactor within a very short time. Therefore, the size of the reactor can be made compact substantially, by the use of such methanogenic bacteria. In addition, the time required for establishing a desired bacterial cell number in the reactor can also be reduced substantially and thus a stable steady state of methane fermentation can be maintained.

Description

  • The present invention relates to a methane fermentation method in which methanogenic bacteria are used and more specifically to a method for carrying out methane fermentation in a reactor for methane fermentation at a high speed within a short period of time in which the concentration of methanogenic bacteria is increased, and the best use of the properties of the methanogenic bacteria is made.
  • Heretofore, there have been known the following 5 bacterial species as methanogenic bacteria belonging to the genus Methanosarcina: Methanosarcina barkeri (see Microbiological Reviews, 1979, Vol. 47, pp. 260-296 and FEMS Microbiology Letters, 1983, Vol. 16, pp. 217-223); Methanosarcina acetivorans (see Applied and Environmental Microbiology, 1984, Vol. 47, No.5, pp. 971-978); Methanosarcina vacuolata (see Microbiology, U.S.S.R., 1979, Vol. 48, pp. 279-285); Methanosarcina thermophila (see International Journal of Systematic Bacteriology, 1985, Vol. 35, No.4, pp. 522-523); and Methanosarcina mazei (see Current Microbiology, 1980, Vol. 3, pp. 321-326). These species can be used for the method of the invention.
  • Besides, methane fermentation methods have been utilized widely for treating waste water and solid waste from the viewpoint of effective use of biomass, biogas production or the like.
  • Nevertheless, the conventionally known methanogenic bacteria used in methane fermentation methods are strictly anaerobic bacteria and show an extremely slow growth rate. For this reason, the use of a large-scale reactor for methane fermentation is required and likewise it takes a long period of time to obtain in the reactor the concentration of the methanogenic bacteria which is required for maintaining a stable steady state of methane fermentation.
  • There has been proposed a method which comprises the step of controlling conditions in the reactor such as pH and temperature for the purpose of improving the efficiency of the foregoing methane fermentation. However, such a control of only the environmental conditions enables such a method to be speeded up only slightly and permits an improvement of efficiency only to a limited level.
  • Furthermore, a method of methane fermentation utilizing organic waste is disclosed, characterized by using methane bacteria such as methanosulcina, methanococcus or methanobacterium and adding lower aliphatic acid or alcohol such as acetic acid, butyric acid, methyl alcohol or ethyl alcohol to the organic waste (see Patent Abstracts of Japan, 1980, Vol. 4, No. 19 (C-73)).
  • In particular, in the methane fermentation methods for treating solid waste and/or waste water, the main substrates are acetic acid and H2/CO2 (among the substrates capable of being assimlated by methanogens, acetic acid and H2/CO2 are exclusively present in such waste). However, the assimilation rate of acetic acid by methanogenic bacteria is very low and this serves as a rate-determining step. Thus, it takes a long period of time to start the methane fermentation reactor and the volume of the reactor must be enlarged. Morever, the reactor is started according to the adaptation-cultivation method using substrates inherent to the bacteria used.
  • Accordingly, an object of the present invention is to provide a methane fermentation method which can provide methane at a high speed and high efficiency and which makes it possible to increase the bacterial concentration in a reactor within a short period of time, utilizing the bacteriological properties of methanogenic bacteria.
  • According to the present invention, there is provided a methane fermentation method which comprises culturing at least one methanogenic bacterium in a culture medium, wherein the methanogenic bacterium is capable of assimilating one or more first substrates such as acetic acid, H2/CO2, or a mixture thereof at a low rate and a second substrate at a high rate, the culture medium containing one or more said first substrates and the culture being carried out in the additional presence of methylamine as the second substrate.
  • The present invention will hereunder be explained in more detail with reference to the accompanying drawing, wherein,
  • Fig. 1 is a diagram illustrating the change in the amount of methane gas generated with time.
    Figure 00040001
    Figure 00050001
    Composition of the Solution of Trace Element
    Component Amount (g/l)
    Ferrous sulfate 0.3
    Cobalt chloride 0.2
    Zinc chloride 0.1
    Boric acid 0.05
    Sodium molybdate 0.2
    Manganese chloride 0.1
    Copper sulfate 0.01
    Aluminum potassium sulfate 0.005
    Nitrilotriacetic acid 2.5
    Nickel chloride 0.5
    Sodium selenite 0.1
    Sodium tungstate 1.0
    Cadmium chloride 0.05
    *): Each numerical value in Table II denotes the content of each component per liter of the solution of trace elements in which the balance was purified water.
    Composition of the Solution of Vitamin
    Component Amount (mg/l)
    Biotin 2
    Folic acid 2
    Pyridoxine 10
    Riboflavin 5
    Thiamine 5
    Pantothenic acid 5
    Cyanocobalamin 0.1
    p-Aminobenzoic acid 5
    Alpha-lipoic acid 5
    *): Each numerical value in Table III denotes the content of each component per liter of the solution of vitamins in which the balance was purified water.
  • The methane fermentation method of the present invention will hereunder be explained in more detail.
  • In the method of the present invention, there are employed methanogenic bacteria which are capable of utilizing at least two substrates and which utilize these substrates at different assimilation rates.
  • Examples of such methanogenic bacteria include those belonging to the genus Methanosarcina. Specific examples of such: methanogenic bacteria are listed in the following Table IV.
  • The method of the present invention produces methane by culturing the aforementioned methanogenic bacteria in the presence of substrates as principal subject of fermentation which are assimilated by the bacteria at a low assimilation rate such as acetic acid, H2/CO2, or a mixture thereof and carrying out the culture or the fermentation in the presence of substrates which are assimilated at a low assimilation rate and of the substrate methylamine which is assimilated at a rate faster than that of the former.
  • For instance, when Methanosarcina acetivorans C2A is cultured at a temperature of 35 to 40°C, the generation time thereof is 24.1 hours for acetic acid as a substrate; 5.2 hours for methanol; and 6.7 to 7.3 hours for methylamine.
  • If acetic acid is used as the substrate which is assimilated at a low rate, methylamine is used as the substrate assimilated at a high rate.
  • The method of the present invention can likewise be carried out in the same manner as above, when Methanosarcina alkaliphilum, (whose generation time at 37°C is 19 hours for H2/CO2; 17 hours for acetic acid; 4 hours for methanol; and 6 hours for methylamine) is used as the methanogenic bacterium. For instance, when H2/CO2, acetic acid or a mixture thereof is used as the substrate which is assimilated at a low rate, methylamine is used as the substrate which is assimilated at a high assimilation rate.
  • The method of the present invention can be performed in the presence of one or more of the substrates such as acetic acid, H2/CO2 or a mixture thereof which are assimilated at a low assimilation rate and of the substrate methylamine which is assimilated at a high assimilation rate, simultaneously.
  • The time for introducing, into a reaction system, the substrate assimilated at a high rate and the amount thereof may vary depending on factors such as the scale of the fermentation bath. For instance, the starting time of the reaction can extremely be reduced by adding it at the beginning of the fermentation.
  • Conditions of fermentation may appropriately be varied depending on the kinds of the methanogenic bacteria and the fermentation may be carried out according to conventional methods.
  • The method of the present invention can be applied to not only the methane fermentation in treating solid waste and waste water but also to the methane fermentation in all the other fields.
  • The methane fermentation method of the present invention makes it possible to increase the bacterial concentration of the methanogenic bacterium in a reactor within a very short time. Therefore, the size of the reactor can be made compact substantially, by the use of such methanogenic bacteria. In addition, the time required for establishing a desired bacterial cell number in the reactor can also be reduced substantially and thus a stable steady state of methane fermentation can be maintained.
    Name of Bacteria (accession No.) Substrate Assimilation Properties
    H2/CO2 HCOOH MeCOOH MeOH MeNH2
    (i) Known methanogens belonging to genus Methanosarcina
    Methanosarcina barkeri MS (DSM 800T) + - + + +
    Methanosarcina barkeri 227 (DSM 1538) + - + + +
    Methanosarcina barkeri UBS (DSM 1311) + - + + +
    Methanosarcina barkeri DM + - + + +
    Methanosarcina barkeri FRI (DSM 2256) + - + + +
    Methanosarcina acetivorans C2A (DSM 2834T) - - + + +
    Methanosarcina vacuolata Z (DSM 1232) + - + + +
    Methanosarcina thermophila TMI (DSM 1825T) - - + + +
    Methanosarcina mazei (DSM 2053) - - + + +
    (ii) Known alkalophilic methanogens
    Methanosarcina alkaliphilum WeN4 + - - - -
    Methanosarcina thermoalkaliphilum Ac60 + - - - -
    Name of Bacteria (accession No.) Morphology Gramstain Optimum Temp °C Optimum pH Generation Time(h)
    (i) Known methanogens belonging to genus Methanosarcina
    Methanosarcina barkeriMS (DSM 800T) sarcina + 40 7.0 12
    Methanosarcina barkeri 227 (DSM 1538) ditto + 35 7.0 24
    Methanosarcina barkeri UBS (DSM 1311) ditto + 30 7.4 30
    Methanosarcina barkeri DM ditto + 37 7.0 28
    Methanosarcina barkeri FRI (DSM 2256) ditto + 35 --- 33
    Methanosarcina acetivorans C2A (DSM 2834T) ditto - 35-40 7.0 5.2
    Methanosarcina vacuolata Z (DSM 1232) ditto + 40 6.5-7.0 ---
    Methanosarcina thermophila TMI (DSM 1825T) ditto + 50 7.5 5
    Methanosarcina mazei (DSM 2053) ditto ± 30-40 6.0-7.0 7.7
    (ii) Known alkalophilic methanogens
    Methanosarcina alkaliphilum WeN4 rods - 37 8.1-9.1 ---
    Methanosarcina thermoalkaliphilum Ac60 ditto --- 58-62 7.5-8.5 ---
    • Example 1
  • Methanosarcina barkeri UBS (DSM 1311) was cultured, for 16 days, in one liter of the media (pH 7.4; Temp. = 37°C) having the compositions listed in Table I and containing 0.8% sodium acetate as the substrate respectively. The results obtained are plotted on Fig. 1.

Claims (3)

  1. A methane fermentation method which comprises culturing at least one methanogenic bacterium in a culture medium, wherein the methanogenic bacterium is capable of assimilating one or more first substrates such as acetic acid, H2/CO2, or a mixture thereof at a low rate and a second substrate at a high rate, the culture medium containing one or more said first substrates and the culture being carried out in the additional presence of methylamine as the second substrate.
  2. The methane fermentation method according to claim 1 wherein the methanogenic bacterium (bacteria) belongs (belong) to the genus Methanosarcina.
  3. The methane fermentation method according to claim 1 or 2 wherein said part of the substrate which is assimilated at a low assimilation rate is acetic acid.
EP19930113598 1988-03-07 1989-03-07 Fermentation method for the fast production of methane Expired - Lifetime EP0604708B1 (en)

Applications Claiming Priority (7)

Application Number Priority Date Filing Date Title
JP53294/88 1988-03-07
JP5329588 1988-03-07
JP63053294A JPH01225480A (en) 1988-03-07 1988-03-07 Alkaliphile methane-producing bacterium
JP5329588A JPH0647120B2 (en) 1988-03-07 1988-03-07 Fast methane fermentation method
JP53295/88 1988-03-07
JP5329488 1988-03-07
EP19890103989 EP0332134B1 (en) 1988-03-07 1989-03-07 Alkalophilic, methanogenic bacteria and fermentation method for the fast production of methane

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EP19890103989 Division EP0332134B1 (en) 1988-03-07 1989-03-07 Alkalophilic, methanogenic bacteria and fermentation method for the fast production of methane

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EP0604708A1 EP0604708A1 (en) 1994-07-06
EP0604708B1 true EP0604708B1 (en) 1999-07-07

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JPH0198474A (en) * 1987-10-09 1989-04-17 Res Dev Corp Of Japan Highly halophilic bacterium capable of producing methane
IE61765B1 (en) * 1990-02-13 1994-11-30 Worsley Alumina Pty Ltd Biological disposal of oxalates
GR1003552B (en) * 1991-03-07 2001-03-13 Worsley Alumina Pty Limited Biological disposal of oxalates
US5863434A (en) * 1994-12-14 1999-01-26 University Of Ottawa/Universite D'ottawa Psychrophilic anaerobic treatment of waste in a sequencing semibatch/batch bioreactor
CA2160311A1 (en) * 1995-10-11 1997-04-12 Bechara Safi Method of extracting light volatile solvents from a gaseous effluent by wet-scrubbing a gaseous effluent and biomethanation of the solvent-rich liquid
US6019900A (en) * 1998-08-03 2000-02-01 The Regents Of The University Of California Single stage denitrification anaerobic digestion
US6299774B1 (en) 2000-06-26 2001-10-09 Jack L. Ainsworth Anaerobic digester system
JP3363445B1 (en) * 2001-04-23 2003-01-08 新田ゼラチン株式会社 Biopsy cell culture method and animal cell culture kit
SE529177E (en) 2005-12-01 2012-12-21 Tekniska Verken Linkoeping Ab Use of an additive for digestion of organic matter
US20090130734A1 (en) * 2006-06-13 2009-05-21 Laurens Mets System for the production of methane from co2
DE102007025155A1 (en) * 2007-05-29 2008-12-04 Is Forschungsgesellschaft Mbh Process for biogas production
US20100248344A1 (en) * 2009-03-27 2010-09-30 Tech V, LLC Methanogenic reactor
US8158378B2 (en) * 2010-02-03 2012-04-17 Guild Associates, Inc. Utilizing waste tail gas from a separation unit biogas upgrade systems as beneficial fuel
CA2823759C (en) * 2011-01-05 2021-05-25 The University Of Chicago Methanothermobacter thermautotrophicus strain and variants thereof
CN102329768B (en) * 2011-09-19 2013-10-16 华东理工大学 Flora construction method for residual oil gasification exploitation of oil deposit
IN2012DE00799A (en) 2012-03-19 2015-08-21 Council Scient Ind Res

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JPS54154597A (en) * 1978-05-22 1979-12-05 Mitsubishi Heavy Ind Ltd Methane fermentation

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EP0604708A1 (en) 1994-07-06
DE68929029D1 (en) 1999-08-12
EP0332134B1 (en) 1994-12-14
US5143835A (en) 1992-09-01
DE68919874T2 (en) 1995-04-20
EP0332134A3 (en) 1990-01-17
DE68919874D1 (en) 1995-01-26
EP0332134A2 (en) 1989-09-13

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